Inline ultrafiltration

Inline ultrafiltration (UF) can significantly increase the recoverable mass of biopharmaceutical products when pool tank volumes are limiting. Using relatively small commercially available ultrafiltration cassettes, a proof‐of‐concept study demonstrates that inline UF can significantly increase recoverable mass in an antibody purification process. With ever‐increasing cell culture titers pushing product masses to higher levels, inline UF offers a relatively easy‐to‐implement and less disruptive alternative to installing larger pool tanks and enables more cost‐effective production utilizing facilities designed for smaller bulk sizes. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Alginate ultrafiltration membranes

Summary A simple method of producing ultrafiltration membranes, using calcium and barium alginates, has been developed. Although restricted in their flux and rejection characteristics these membranes offer a cheap model system for studying the fouling of hydrophilic membrane surfaces. The method is reproducible, and with suitable modification allows the membranes to be dried and reconstituted with little effect on performance.     

Linear scale ultrafiltration

Tangential flow filtration has traditionally been scaled up by maintaining constant the filtrate volume to membrane surface area ratio, membrane material and pore size, channel height, flow path geometry and retentate and filtrate pressures. Channel width and the number of channels have been increased to provide increased membrane area. Several other parameters, however, have not been maintained constant. A new comprehensive methodology for implementation of linear scale up and scale down of tangential flow filtration processes has been developed. Predictable scale up can only be achieved by maintaining fluid dynamic parameters which are independent of scale. Fluid dynamics are controlled by operating parameters (feed flow rate, retentate pressure, fed batch ratio and temperature), geometry (channel length, height, turbulence promoter and entrance/exit design), materials (membrane, turbulence promoter, and encapsulant compression), and system geometry (flow distribution). Cassette manufacturing procedures and tolerances also play a significant role in achieving scale independent performance. Extensive development work in the aforementioned areas has resulted in the successful implementation of linear scale up of ultrafiltration processes for recovery of human recombinant DNA derived pharmaceuticals. A 400-fold linear scale up has been achieved without intermediate pilot scale tests. Scale independent performance has a direct impact on process yield, protein quality and product economics and is therefore particularly important in the biotechnology industry. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 737-746, 1997.     

Hollow-fibre fermenter using ultrafiltration

Summary A novel bioreactor with hollow fibres was developed to facilitate substrate transfer across membrane walls as well as to retain a continuous cell growth in the shell side. Ultrafiltration was induced through membrane by pressurizing feed solution to the inside of a hollow fibre with inlet and outlet pumps. The ultrafiltrate accumulated outside the hollow fibres was recirculated through a reservoir where a part of solution containing cells and substrate was removed to keep the level of reservoir solution constant. Ethanol production by Saccharomyces cerevisiae was carried out to test the feasibility of this reactor. The productivity of this reactor was compared with that of a continuous stirred tank reactor (CSTR).     

Self-cleaning membranes for ultrafiltration

In order to reduce the severe flux losses encountered during ultrafiltration of protein solutions, proteases were immobilized on Ultrafiltration membranes to hydrolyze the deposited solute molecules. Over a standard 22 hr run 25 to 78% improvement in cumulative permeate yield was obtained when processing 0.5% albumin or hemoglobin. It was also demonstrated that the flux enhancements were due to the biochemical action of the absorbed protease and not to its physical effect as a prefilter coat. with the aid of a model retardation of gel formation mechanism was demonstrated. Economics of the system were shown to be favorable, improving the rate of return on capital investment up to 50% by reduction of the total membrane area of the plant.     

Kinetics of ultrafiltration hemodialysis

The expressions of Wolfet al. (1951) and Renkin (1956) for the kinetics of artificial kidneys are generalized to include the effects of filtration. IfB is the bath volume,b the relevant volume of distribution,f the filtration rate,t the time, andA ₀,B ₀,b ₀ representA, B, andb at timet=0, then the plasma concentrationA is given by

$$\frac{A}{{A_0 }} = \frac{{B_0 }}{{B_0 + b_0 }}e^{ - \frac{{\left( {B_0 + b_0 } \right)}}{{B_0 }}\frac{{D_f }}{{b_0 }}K\left( {ft} \right)t} + \frac{{b_0 }}{{B_0 + b_0 }}$$     

Glomerular permselection: shape and flow

The selective permeability of the glomerular basement membrane to macromolecules is a function of the size and charge of the macromolecule. Evidence suggests that shape may also be a factor. The orientation of macromolecules in solution is dependent on their size, shape, and frictional interactions with moving solvent molecules. The spaces between the glomerular visceral epithelial cells (slit pores) may produce a non-uniform distribution of fluid flow within the basement membrane, and this non-uniformity may increase during disease. This report is of a model that relates the filtration of rigid prolate ellipsoidal (cigar) shaped macromolecules to the size and shape of the filter and to the velocity of solvent flow. The calculations, using published macromolecular and glomerular parameters correspond well to published data. The glomerular visceral epithelial cell, by altering the number, size and distribution of the intercellular spaces, may regulate the passage of ellipsoidal shaped macromolecules, such as albumin and IgG, into and through glomerular structures.     

Glomerular compromise in mercuric chloride-induced nephrotoxicity

We have examined the effects of mercuric chloride on renal glomerular structure. Isolated glomeruli from mercury-treated rats (HgCl₂, 5 mg/kg body wt, s.c.) 1 hour post injection presented a diminished cross-sectional area as compared with control glomeruli [control (μm²) = 26,310 ± 2,545, HgCl₂ (μm²) = 18,474 ± 1,828] and higher glomerular calcium content (control = 23 ± 6 nmoles/mg prot, HgCl₂ = 43 ± 7 nmoles/mg prot). Renal sections prepared for immunohistochemical and histochemical analysis showed larger deposits of fibronectin and lipids and enhanced cellularity in glomerular structures from HgCl₂-treated rats. Moreover, mieloperoxidase activity measured in isolated glomeruli were also increased as compared with control preparations [MPO (U/mg prot): control = 59 ± 7, HgCl₂ = 134 ± 10]. When the animals were studied 24 hours post HgCl₂ injection, glomerular cross-sectional area values were not different from control values (25,276 ± 1,983 μm²), while calcium contents were higher than values observed 1 hour after treatment (92 ± 9 nmoles/mg prot). A similar pattern was observed in fibronectin deposits. Hypercellularity in glomerular structures and the higher mieloperoxidase levels were maintained at this time (MPO HgCl₂-rats 24 h = 148 ± 31 U/mg prot). The effects observed in this study are consistent with an inflammatory response in the glomerular structure of HgCl₂-treated rats that could explain the altered renal function described in previous reports in our laboratory. © 1997 John Wiley & Sons, Inc.     

超滤法提纯万古霉素的应用

采用Ultra-flo超滤系统提纯未经任何预处理的万古霉素发酵液。结果表明:万古霉素收率由传统工艺(板框加压过滤)的87%提高到94%,滤液的透光度比传统工艺提高了25%;系统平均膜通量可达120L/(m2.h);被污染的膜经清洗后与新膜没有明显差异;合理加水量为投料量的2.5倍。Ultra-flo超滤系统完全能代替传统工艺。